AU2002222115B2 - Method of making particles for use in a pharmaceutical composition - Google Patents

Method of making particles for use in a pharmaceutical composition Download PDF

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Publication number
AU2002222115B2
AU2002222115B2 AU2002222115A AU2002222115A AU2002222115B2 AU 2002222115 B2 AU2002222115 B2 AU 2002222115B2 AU 2002222115 A AU2002222115 A AU 2002222115A AU 2002222115 A AU2002222115 A AU 2002222115A AU 2002222115 B2 AU2002222115 B2 AU 2002222115B2
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Prior art keywords
particles
active particles
composite active
material
method according
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AU2002222115A1 (en
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Matthew Michael James Green
David Alexander Vodden Morton
John Nicholas Staniforth
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Vectura Ltd
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Vectura Ltd
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Priority to GB0029261.5 priority Critical
Priority to GB0029261A priority patent/GB0029261D0/en
Priority to GB0030946A priority patent/GB0030946D0/en
Priority to GB0030946.8 priority
Priority to WOPCT/GB01/01606 priority
Priority to PCT/GB2001/001606 priority patent/WO2001076575A2/en
Priority to GB0124010.0 priority
Priority to GB0124010A priority patent/GB0124010D0/en
Priority to PCT/GB2001/005315 priority patent/WO2002043701A2/en
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL, OR TOILET PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/0012Galenical forms characterised by the site of application
    • A61K9/007Pulmonary tract; Aromatherapy
    • A61K9/0073Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy
    • A61K9/0075Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy for inhalation via a dry powder inhaler [DPI], e.g. comprising micronized drug mixed with lactose carrier particles
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL, OR TOILET PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/0012Galenical forms characterised by the site of application
    • A61K9/007Pulmonary tract; Aromatherapy
    • A61K9/0073Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy
    • A61K9/008Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy comprising drug dissolved or suspended in liquid propellant for inhalation via a pressurized metered dose inhaler [MDI]
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL, OR TOILET PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/141Intimate drug-carrier mixtures characterised by the carrier, e.g. ordered mixtures, adsorbates, solid solutions, eutectica, co-dried, co-solubilised, co-kneaded, co-milled, co-ground products, co-precipitates, co-evaporates, co-extrudates, co-melts; Drug nanoparticles with adsorbed surface modifiers
    • A61K9/145Intimate drug-carrier mixtures characterised by the carrier, e.g. ordered mixtures, adsorbates, solid solutions, eutectica, co-dried, co-solubilised, co-kneaded, co-milled, co-ground products, co-precipitates, co-evaporates, co-extrudates, co-melts; Drug nanoparticles with adsorbed surface modifiers with organic compounds
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL, OR TOILET PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1617Organic compounds, e.g. phospholipids, fats

Description

WO 02/43701 PCT/GB01/05315 1 Method of making particles for use in a pharmaceutical composition The present invention relates to particles and to methods of making particles. In particular, the invention relates to methods of making composite active particles comprising a pharmaceutically active material for inhalation.

It is known to administer to patients drugs in the form of fine particles (active particles). For example, in pulmonary administration a particulate medicament composition is inhaled by the patient. Pulmonary administration is particularly suitable for medicaments which are intended to cure or alleviate respiratory conditions such as asthma and for medicaments which are not suitable for oral ingestion such as certain biological macromolecules. Known devices for the administration of drugs to the respiratory system include pressurised metered dose inhalers (pMDI's) and dry powder inhalers (DPI's).

The size of the active particles is of great importance in determining the site of the absorption. In order that the particles be carried deep into the lungs, the particles must be very fine, for example having a mass median aerodynamic diameter of less than 10m. Particles having aerodynamic diameters greater than l0ym are likely to impact the walls of the throat and generally do not reach the lung. Particles having aerodynamic diameters in the range of 5lm to 0.5pm will generally be deposited in the respiratory bronchioles whereas smaller particles having aerodynamic diameters in the range of 2 to 0.05im are likely to be deposited in the alveoli.

Such small particles are, however, thermodynamically unstable due to their high surface area to volume ratio, which provides significant excess surface free energy and encourages particles to agglomerate. In the inhaler, agglomeration of small particles and adherence of particles to the walls of the WO 02/43701 PCT/GB01/05315 2 inhaler are problems that result in the active particles leaving the inhaler as large agglomerates or being unable to leave the inhaler and remaining adhered to the interior of the inhaler.

In an attempt to improve that situation, dry powders for use in dry powder inhalers often include particles of an excipient material mixed with the fine particles of active material. Such particles of excipient material may be coarse, for example, having mass median aerodynamic diameters greater than 90V, (such coarse particles are referred to as carrier particles) or they may be fine.

The step of dispersing the active particles from other active particles and from particles of excipient material, if present, to form an aerosol of fine active particles for inhalation is significant in determining the proportion of the dose of active material which reaches the desired site of absorption in the lungs. In order to improve the efficiency of that dispersal it is known to include in the composition additive materials. Such additive materials are thought to reduce the attractive forces between the particles thereby promoting their dispersal. Compositions comprising fine active particles and additive materials are disclosed in WO 97/03649.

Fine particles of active material suitable for pulmonary administration have often been prepared by milling, for example, jet milling. However, once the particles reach a minimum size referred to as the critical size, they re-combine at the same rate as being fractured, or do not fracture effectively and therefore do not reduce further in size.

Thus, manufacture of fine particles by milling can require much effort and there are factors which consequently place limits on the minimum size of particles of active material which can be achieved, in practice, by such milling processes.

Summary of the invention According to a first aspect, the present invention provides a method for making composite active particles for use in a pharmaceutical composition for pulmonary administration, the method comprising a milling step in which particles of active material are milled in the presence of particles of an additive material so as to ensure a sufficient _break-up of agglomerates of both active material and additive material, dispersal and even distribution of the additive material over the active material, and so that the particles of additive material become fused to the surface of the particles of active material, wherein the additive material is suitable for the promotion of the dispersal of 0 the composite active particles upon actuation of an inhaler.

(Ni According to a second aspect, the present invention provides composite active particles for use in a pharmaceutical composition as made by the method according to the first aspect.

According to a third aspect, the present invention provides composite active particles for use in a pharmaceutical composition for pulmonary administration, each composite active particle comprising a particle of active material and additive material dispersed, evenly distributed and fused on the surface of that particle of active material, the composite active particles having a mass median aerodynamic diameter of not more than 10pm and the additive material being suitable for the promotion of the dispersal of the composite active particles upon actuation of a delivery device.

According to a fourth aspect, the present invention provides a pharmaceutical composition comprising composite active particles as made by a method according to the first aspect or composite active particles according to the second or third aspect.

WO 02/43701 PCT/GB01/05315 3 The present invention provides in a first aspect a method for making composite active particles for use in a pharmaceutical composition for pulmonary administration, the method comprising a milling step in which particles of active material are milled in the presence of particles of an additive material which is suitable for the promotion of the dispersal of the composite active particles upon actuation of an inhaler.

The method of the invention will, in general, produce composite active particles. The composite active particles are very fine particles of active material which have, upon their surfaces, an amount of the additive material. The additive material is preferably in the form of a coating on the surfaces of the particles of active material. The coating may be a discontinuous coating. The additive material may be in the form of particles adhering to the surfaces of the particles of active material. As explained below, at least some of the composite active particles may be in the form of agglomerates.

When the composite active particles are included in a pharmaceutical composition the additive material promotes the dispersal of the composite active particles on administration of that composition to a patient, via actuation of an inhaler.

("Actuation of an inhaler refers to the process during which a dose of the powder is removed from its rest position in the inhaler. That step takes place after the powder has been loaded into the inhaler ready for use.) The effectiveness of that promotion of dispersal has been found to be enhanced in comparison to a composition made by simple blending of similarly sized particles of active material with additive material.

The presence of the additive material on the surfaces of the particles of active material may confer controlled or WO 02/43701 PCT/GB01/05315 4 delayed release properties and may provide a barrier to moisture.

It has also been found that the milling of the particles of active material in the presence of an additive material produces significantly smaller particles and/or requires less time and less energy than the equivalent process carried out in the absence of the additive material. Using the method of the invention, it has been possible to produce composite active particles which have a mass median aerodynamic diameter (MMAD) or a volume median diameter (VMD) of less than lm. It is often not possible to make such small particles by other milling methods.

It is known that a milling process will tend to generate and increase the level of amorphous material on the surfaces of the milled particles thereby making them more cohesive. In contrast, the composite active particles of the invention will often be found to be less cohesive after the milling treatment.

The word "milling" as used herein refers to any mechanical process which applies sufficient force to the particles of active material that it is capable of breaking coarse particles (for example, particles of mass medium aerodynamic diameter greater than 100Am) down to fine particles of mass median aerodynamic diameter not more than 50m or which applies a relatively controlled compressive force as described below in relation to the Mechano-Fusion and Cyclomix methods. It has been found that processes such as blending which do not apply a high degree of force are not effective in the method of the invention. It is believed that is because a high degree of force is required to separate the individual particles of active material and to break up tightly bound agglomerates of the active particles such that effective mixing and effective application of the additive material to the surfaces of those particles is achieved. It is WO 02/43701 PCT/GB01/05315 believed that an especially desirable aspect of the milling process is that the additive material may become deformed in the milling and may be smeared over or fused to the surfaces of the active particles. It should be understood, however, that in the case where the particles of active material are already fine, for example, having a mass median aerodynamic diameter below 20y prior to the milling step, the size of those particles may not be significantly reduced. The important thing is that the milling process applies a sufficiently high degree of force or energy to the particles.

The method of the invention generally involves bringing the additive particles into close contact with the surfaces of the active particles. In order to achieve coated particles, a degree of intensive mixing is required to ensure a sufficient break-up of agglomerates of both constituents, dispersal and even distribution of additive over the host active particles.

Where the additive particles are very small (typically 1 micron), generally less work is required, firstly as it is not required to break or deform but only to deagglomerate, distribute and embed the additive particles onto the active particle and secondly because of the naturally high surface energies of such small additive particles. It is known that where two powder components are mixed and the two components differ in size, there is a tendency for the small particles to adhere to the large particles (to form so called 'ordered mixes'). The short range Van der Waals interactions for such very fine components may be sufficient to ensure adhesion.

However, where both additive and active particles are very fine (for example less than 5 microns) a substantial degree of mixing will be required to ensure a sufficient break-up of agglomerates of both constituents, dispersal and even distribution of additive particles over the active particles as noted above. In some cases a simple contact adhesion may be insufficient and a stronger embedding or fusion of additive WO 02/43701 PCT/GB01/05315 particles onto active particles is required to prevent segregation, or to enhance the structure and functionality of the coating.

Where the additive particles are not so small as to be sufficiently adhered by Van der Waals forces alone, or where there are advantages to distorting and/or embedding the additive particles substantially onto the host active particle, a greater degree of energy is required from the milling. In this case, the additive particles should experience sufficient force to soften and/or break, to distort and to flatten them. These processes are enhanced by the presence of the relatively harder active particles which act as a milling media as well as a de-agglomerating media for such processes. As a consequence of this process the additive particles may become wrapped around the core active particle to form a coating. These processes are also enhanced by the application of a compressive force as mentioned above.

As a consequence of the milling step, complete or partial, continuous or discontinuous, porous or non-porous coatings may be formed. The coatings originate from a combination of active and additive particles. They are not coatings such as those formed by wet processes that require dissolution of one or both components. In general, such wet coating processes are likely to be more costly and more time consuming than the milling process of the invention and also suffer from the disadvantage that it is less easy to control the location and structure of the coating.

A wide range of milling devices and conditions are suitable for use in the method of the invention. The milling conditions, for example, intensity of milling and duration, should be selected to provide the required degree of force.

Ball milling is a preferred method. Centrifugal and planetary ball milling are especially preferred methods. Alternatively, a high pressure homogeniser may be used in which a fluid WO 02/43701 PCT/GB01/05315 7 containing the particles is forced through a valve at high pressure producing conditions of high shear and turbulence.

Shear forces on the particles, impacts between the particles and machine surfaces or other particles and cavitation due to acceleration of the fluid may all contribute to the fracture of the particles and may also provide a compressive force.

Such homogenisers may be more suitable than ball mills for use in large scale preparations of the composite active particles.

Suitable homogensiers include EmulsiFlex high pressure homogenisers which are capable of pressures up to 4000 Bar, Niro Soavi high pressure homogenisers (capable of pressures up to 2000 Bar), and Microfluidics Microfluidisers (maximum pressure 2750 Bar). The milling step may, alternatively, involve a high energy media mill or an agitator bead mill, for example, the Netzch high energy media mill, or the DYNO-mill (Willy A. Bachofen AG, Switzerland). Alternatively the milling may be a dry coating high energy process such as a Mechano- Fusion system (Hosokawa Micron Ltd) or a Hybridizer (Nara).

Other possible milling devices include air jet mills, pin mills, hammer mills, knife mills, ultracentrifugal mills and pestle and mortar mills.

Especially preferred methods are those involving the Mechano-Fusion, Hybridiser and Cyclomix instruments.

Preferably, the milling step involves the compression of the mixture of active and additive particles in a gap (or nip) of fixed, predetermined width (for example, as in the Mechano- Fusion and Cyclomix methods described below).

Some preferred milling methods will now be described in greater detail.

Mechano-Fusion: As the name suggests, this dry coating process is designed to mechanically fuse a first material onto a second material. The first material is generally smaller and/or softer than the second. The Mechano-Fusion and Cyclomix WO 02/43701 PCT/GB01/05315 8 working principles are distinct from alternative milling techniques in having a particular interaction between inner element and vessel wall, and are based on providing energy by a controlled and substantial compressive force.

The fine active particles and the additive particles are fed into the Mechano-Fusion driven vessel, where they are subject to a centrifugal force and are pressed against the vessel inner wall. The powder is compressed between the fixed clearance of the drum wall and a curved inner element with high relative speed between drum and element. The inner wall and the curved element together form a gap or nip in which the particles are pressed together. As a result the particles experience very high shear forces and very strong compressive stresses as they are trapped between the inner drum wall and the inner element (which has a greater curvature than the inner drum wall). The particles violently collide against each other with enough energy to locally heat and soften, break, distort, flatten and wrap the additive particles around the core particle to form a coating. The energy is generally sufficient to break up agglomerates and some degree of size reduction of both components may occur. Embedding and fusion of additive particles onto the active particles may occur, and may be facilitated by the relative differences in hardness (and optionally size) of the two components. Either the outer vessel or the inner element may rotate to provide the relative movement. The gap between these surfaces is relatively small, and is typically less than 10mm and is preferably less than more preferably less than 3mm. This gap is fixed, and consequently leads to a better control of the compressive energy than is provided in some other forms of mill such as ball and media mills. Also, in general, no impaction of milling media surfaces is present so that wear and consequently contamination are minimised. The speed of rotation may be in the range of 200 to 10,000rpm. A scraper WO 02/43701 PCT/GB01/05315 9 may also be present to break up any caked material building up on the vessel surface. This is particularly advantageous when using fine cohesive starting materials. The local temperature may be controlled by use of a heating/cooling jacked built into the drum vessel walls. The powder may be re-circulated through the vessel.

Cyclomix Method (Hosokawa Micron): The Cyclomix comprises a stationary conical vessel with a fast rotating shaft with paddles which move close to the wall. Due to the high rotational speed of the paddles, the powder is propelled towards the wall, and as a result the mixture experiences very high shear forces and compressive stresses between wall and paddle. Such effects are similar to the Mechano-Fusion as described above and may be sufficient to locally heat and soften, to break, distort, flatten and wrap the additive particles around the active particles to form a coating. The energy is sufficient to break up agglomerates and some degree of size reduction of both components may also occur depending on the conditions and upon the size and nature of the particles.

Hybridiser Method: This is a dry process which can be described as a product embedding or filming of one powder onto another. The fine active particles and fine or ultra fine additive particles are fed into a conventional high shear mixer pre-mix system to form an ordered mixture. This powder is then fed into the Hybridiser. The powder is subjected to ultra-high speed impact, compression and shear as it is impacted by blades on a high speed rotor inside a stator vessel, and is re-circulated within the vessel. The active and additive particles collide with each other. Typical speeds of rotation are in the range of 5,000 to 20,000rpm. The relatively soft fine additive particles experience sufficient impact force to soften, break, distort, flatten and wrap around the active particle to form a WO 02/43701 PCT/GB01/05315 10 coating. There may also be some degree of embedding into the surface of the active particles.

Other preferred methods include ball and high energy media mills which are also capable of providing the desired high shear force and compressive stresses between surfaces, although as the clearance gap is not controlled, the coating process may be less well controlled than for Mechano-Fusion milling and some problems such as a degree of undesired reagglomeration may occur. These media mills may be rotational, vibrational, agitational, centrifugal or planetary in nature.

It has been observed in some cases that when ball milling active particles with additive material, a fine powder is not produced. Instead the powder was compacted on the walls of the mill by the action of the mill. That has inhibited the milling action and prevented the preparation of the composite active particles. That problem occurred particularly when certain additive materials were used, in cases where the additive material was present in small proportions (typically in cases where the milling balls were relatively small (typically <3mm), in cases where the milling speed was too slow and where the starting particles were too fine. To prevent this occurring it is advantageous to ball mill in a liquid medium. The liquid medium reduces the tendency to compaction, assists the dispersal of additive material and improves any milling action.

It has been found to be preferable to use a large number of fine milling balls, rather than fewer heavy balls. The finer balls perform a more efficient co-milling action.

Preferably the balls have a diameter of less than advantageously less than 2mm. Liquid media are preferred which do not dissolve the active material and which evaporate rapidly and fully, for example non-aqueous liquids such as diethylether, acetone, cyclohexane, ethanol, isopropanol or dichloromethane. Liquid media are preferred which are non WO 02/43701 PCT/GB01/05315 11 flammable, for example dichloromethane and fluorinated hydrocarbons, especially fluorinated hydrocarbons which are suitable for use as propellants in inhalers.

Pestle and mortar mills are other mills which also provide a very high shear force and compressive stresses between surfaces.

Mechano-Micros and Micros mills made by Nara (where particles are compressed by rotating grinding rings) may also be used. Mills referred to impact mixers, attrition mills, pin mills and disc mills may also be used.

The mass median aerodynamic diameter of the particles of active material may be substantially reduced during the milling step especially when the active material is in the form of coarse particles prior to the milling step. The mass median aerodynamic diameter (MMAD) of the particles of active material may be reduced by at least 10%, by at least 50%, or by at least 70% during the milling step depending on the milling conditions and the MMAD of the active particles prior to the milling step.

Advantageously, after the milling step, the MMAD of the active particles is less than 94m, preferably less then 4gm and more preferably less then 2pm.

In a similar way, where the additive material is in the form of coarse particles prior to the milling step, their MMAD will be substantially reduced during the milling step. The MMAD of the particles of additive material may be reduced by at least 10%, at least 50% or at least 70% during the milling step, depending on the milling conditions and on the MMAD of the particles of additive material before the milling step.

The size of the additive particles after the milling step is preferably significantly less than the size of the active particles, to enable the additive materials to more effectively coat the surfaces of the active particles. In practice, that difference in size between the active particles WO 02/43701 PCT/GB01/05315 12 and additive particles is likely to be achieved as a consequence of the milling because the additive material will usually be more easily fractured or deformed than the active material and so will be broken into smaller particles than the active material. As noted above, the particles of additive material preferably become smeared over or fused to the surfaces of the particles of active material, thereby forming a coating which may be substantially continuous or discontinuous. Where the coating is discontinuous, it preferably covers, on average, at least 50% (that is, at least of the total surface area of the active particles will be covered by additive material), more advantageously at least and most preferably at least 90% of the surfaces of the active particles. The coating is preferably on average less than 1gm, more preferably less than 0.5gm and most preferably less than 200nm thick.

The milling step may be carried out in a closed vessel, for example in a ball mill or a Mechano-Fusion device. The use of a closed vessel prevents loss of ultrafine particles or vapour of the additive material which has been found to occur in jet milling or other open processes. Preferably, the milling is not jet milling (micronisation) The milling may be wet milling, that is, the milling step may be carried out in the presence of a liquid. That liquid medium may be high or low volatility and of any solid content as long as it does not dissolve the active particles to any significant degree and its viscosity is not so high that it prevents effective milling. The liquid medium preferably is not aqueous. The liquid is preferably one in which the additive material is substantially insoluble but some degree of solubility may be acceptable as long as there is sufficient additive material present that undissolved particles of additive material remain. The presence of a liquid medium helps to prevent compacting of the particles of active WO 02/43701 PCT/GB01/05315 13 material on the walls of the vessel and may also allow the more even spreading of the additive material on the surface of the particles of active material as compared to dry milling.

It has been found that the Mechano-Fusion and Cyclomix techniques referred to above often provide the composite active particles as individual, that is, unagglomerated composite active particles. That is in contrast to less controlled methods such as ball milling, which have been found to often produce the composite active particles in the form of agglomerated composite active particles.

The mass median aerodynamic diameter of the composite active particles is preferably not more than 10pm, and advantageously it is not more than 5Am, more preferably not more than 3m and most preferably not more than 1/m.

Accordingly, advantageously at least 90% by weight of the composite active particles have a diameter of not more than advantageously not more than 5sm, preferably not more than 3pm and more preferably not more than lym.

Advantageously, after the milling step, the active particles will be of a suitable size for inhalation to the desired part of the lung, for example, having an MMAD in the range of 3 to 0.lm for absorption in the deep lung, 5 to 0.5pm for absorption in the respiratory bronchioles, 10 to 2pm for delivery to the higher respiratory system and 2 to 0.05pm for delivery to the alveoli. Accordingly, advantageously the diameter of at least 90% by weight of the composite active particles have an aerodynamic diameter in the range of 3 to 0.lm, preferably 5 to 0.5pm, advantageously 10 to 2/m, and especially advantageously 2 to 0.05pm. The MMAD of the active particles will not normally be lower than 0.01m.

As mentioned above, the composite active particles produced after the milling step may be of a suitable size for delivery to the desired part of the respiratory system.

WO 02/43701 PCT/GB01/05315 14 However, the composite active particles may be smaller than that suitable size or at least some of the composite active particles may, after the milling step, be in the form of agglomerates which are larger than the suitable size. The method therefore preferably also comprises, after the milling step, a processing step in which the degree of agglomeration of the composite active particles is changed. The processing step may be an agglomeration step in which the particles of active material agglomerate to form agglomerated composite active particles. In that way agglomerates of a size tailored to the requirement may be produced. Whilst any method of agglomeration can be used, for example, granulation, preferably, the composite active particles are agglomerated in a drying step (as described below) to form agglomerated composite active particles. Preferably, the agglomeration step is a spray drying step. The spray drying conditions may be selected to produce droplets having a desired size in the range of 1000gm to 0.5pm. The size of the agglomerates produced will depend largely on the concentration of the composite active particles in the spray feed and the droplet size. Other materials, for example, binders may be included in the spray feed. Where the milling step involves wet milling, the suspension or slurry may be spray dried directly after the milling step. Agglomeration may also be conducted in a fluid bed dryer or granulator.

Where, after the milling step, at least some of the composite active particles are in the form of agglomerates and it is desired to break those agglomerates down or to reduce their size, the processing step may be a deagglomeration step.

The deagglomeration step may involve mechanical breaking up of the unwanted agglomerates, for example, by forcing them through a sieve or by subjecting them to a treatment in a dry fluidised bed, a jet mill, a ball mill or other form of milling device. The intensity and/or duration of that WO 02/43701 PCT/GB01/05315 15 treatment step will, in general, be less that of the milling step. The deagglomeration step may also be a spray drying step because, whilst spray drying as a drying step is particularly useful in preparing agglomerated composite active particles, by appropriate control of the conditions it is possible to produce the composite active particles largely as single particles rather than as agglomerates.

The term "agglomerated composite active particles" refers to particles which consist of more than one composite active particle, those composite active particles being adhered to each other. Where the agglomerated particles are for inhalation they will preferably have a MMAD which renders them suitable for deposition in the desired part of the lung.

Preferably, the method comprises, after the milling step, a drying step in which a mixture of the composite active particles and a liquid is dried to remove the liquid. The mixture may be in the form of a slurry or suspension. During the drying step, especially when spray drying is used, the degree of agglomeration of the composite active particles may change, in which case the drying step is the same step as the processing step mentioned above. However, the drying step may be included for other reasons, for example, when the milling is wet milling, and it is desired to produce the composite active particles as a dry powder.

The drying step may involve filtration followed by drying, or evaporation of the liquid. Preferably, the drying step is a spray drying step. Alternatively, the liquid may be evaporated slowly or the drying step may be a freeze drying step.

The milling is preferably dry, that is to say, there is no liquid present during the milling and the mixture to be milled is in the form cf a dry particulate. In that case, liquid may be added after the milling step, usually in order WO 02/43701 PCT/GB01/05315 16 that a drying step be used to form agglomerated composite active particles, as described above.

Advantageously, the milling step is carried out at a reduced temperature, for example, below 10 0 C and preferably below 0°C. Such low temperature conditions may increase the efficiency of the milling step and/or reduce decomposition of the active material.

The optimum amount of additive material will depend on the chemical composition and other properties of the additive material and upon the nature of the active material and/or excipient material. In general, the amount of additive material in the composite particles will be not more than by weight, based on the weight of the active material and/or excipient material. However, it is thought that for most additive materials the amount of additive material should be in the range of 40% to 0.25%, preferably 30% to more preferably 20% to based on the total weight of the additive material and the active material being milled. In general, the amount of additive material is at least 0.01% by weight based on the weight of the active material.

The terms "additive particles" and "particles of additive material" are used interchangeably herein. The additive particles comprise one or more additive materials. Preferably, the additive particles consist essentially of the additive material.

Advantageously the additive material is an anti-adherent material and will tend to decrease the cohesion between the composite active particles and between the composite active particles and any other particles present in the pharmaceutical composition.

Advantageously the additive material is an anti-friction agent (glidant) and will give better flow of the pharmaceutical composition in, for example, a dry powder inhaler which will lead to a better dose reproducibility.

WO 02/43701 PCT/GB01/05315 17 Where reference is made to an anti-adherent material, or to an anti-friction agent, the reference is to include those materials which are able to decrease the cohesion between the particles, or which will tend to improve the flow of powder in an inhaler, even though they may not usually be referred to as anti-adherent material or an anti-friction agent. For example, leucine is an anti-adherent material as herein defined and is generally thought of as an anti-adherent material but lecithin is also an anti-adherent material as herein defined, even though it is not generally thought of as being anti-adherent, because it will tend to decrease the cohesion between the composite active particles and between the composite active particles and any other particles present in the pharmaceutical composition.

The additive material may include a combination of one or more materials.

It will be appreciated that the chemical composition of the additive material is of particular importance.

Preferably, the additive material is a naturally occurring animal or plant substance.

Advantageously, the additive material includes one or more compounds selected from amino acids and derivatives thereof, and peptides and derivatives thereof. Amino acids, peptides and derivatives of peptides are physiologically acceptable and give acceptable release of the active particles on inhalation.

It is particularly advantageous for the additive material to comprise an amino acid. The additive material may comprise one or more of any of the following amino acids: leucine, isoleucine, lysine, valine, methionine, phenylalanine. The additive may be a salt or a derivative of an amino acid, for example aspartame or acesulfame K. Preferably, the additive particles consist substantially of an amino acid, more preferably of leucine, advantageously L-leucine. The D- and WO 02/43701 PCT/GB01/05315 18 DL-forms may also be used. As indicated above, leucine has been found to give particularly efficient dispersal of the active particles on inhalation.

The additive material may include one or more water soluble substances. This helps absorption of the substance by the body if the additive reaches the lower lung. The additive material may include dipolar ions, which may be zwitterions.

Alternatively, the additive material may comprise a phospholipid or a derivative thereof. Lecithin has been found to be a good material for the additive material.

Preferably, the additive material comprises a metal stearate, or a derivative thereof, for example, sodium stearyl fumarate or sodium stearyl lactylate. Advantageously, the additive material comprises a metal stearate. For example, zinc stearate, magnesium stearate, calcium stearate, sodium stearate or lithium stearate. Preferably, the additive material comprises magnesium stearate.

The additive material may include or consist of one or more surface active materials, in particular materials that are surface active in the solid state, which may be water soluble, for example lecithin, in particular soya lecithin, or substantially water insoluble, for example solid state fatty acids such as oleic acid, lauric acid, palmitic acid, stearic acid, erucic acid, behenic acid, or derivatives (such as esters and salts) thereof such as glyceryl behenate. Specific examples of such materials are: phosphatidylcholines, phosphatidylethanolamines, phosphatidylglycerols and other examples of natural and synthetic lung surfactants; lauric acid and its salts, for example, sodium lauryl sulphate, magnesium lauryl sulphate; triglycerides such as Dynsan 118 and Cutina HR; and sugar esters in general.

Other possible additive materials include sodium benzoate, hydrogenated oils which are solid at room temperature, talc, titanium dioxide, aluminium dioxide, WO 02/43701 PCT/GB01/05315 19 silicon dioxide and starch.

The additive material preferably comprises one or more materials selected from the group consisting of amino acids, lecithins, phospholipids, sodium stearyl fumarate, glyceryl behenate and metal stearates (especially magnesium stearate).

The terms "active particles" and "particles of active material" are used interchangeably herein. The active particles referred to throughout the specification will comprise one or more pharmacologically active agents. The active particles advantageously consist essentially of one or more pharmacologically active agents. Suitable pharmacologically active agents may be materials for therapeutic and/or prophylactic use. Active agents which may be included in the formulation include those products which are usually administered orally by inhalation for the treatment of disease such as respiratory disease, for example, S-agonists.

The active particles may comprise at least one 9 2 -agonist, for example one or more compounds selected from terbutaline, salbutamol, salmeterol and formetorol. If desired, the active particles may comprise more than one of those active agents, provided that they are compatible with one another under conditions of storage and use. Preferably, the active particles are particles of salbutamol sulphate. References herein to any active agent is to be understood to include any physiologically acceptable derivative. In the case of the

B

2 -agonists mentioned above, physiologically acceptable derivatives include especially salts, including sulphates.

The active particles may be particles of ipatropium bromide.

The active particles may include a steroid, which may be beclomethasone dipropionate or may be Fluticasone. The active principle may include a cromone which may be sodium cromoglycate or nedocromil. The active principle may include WO 02/43701 PCT/GB01/05315 20 a leukotriene receptor antagonist.

The active particles may include a carbohydrate, for example heparin.

The active particles may advantageously comprise a pharmacologically active agent for systemic use and advantageously they are capable of being absorbed into the circulatory system via the lungs. For example, the active particles may comprise peptides or polypeptides such as Dnase, leukotrienes or insulin. The pharmaceutical compositions of the invention may in particular have application in the administration of insulin to diabetic patients, preferably avoiding the normally invasive administration techniques used for that agent. The composite active particles could also be used for the local administration of other agents for example for pain relief analgesics such as Fentanyl or dihydroergotamine which is used for the treatment of migraine), anti cancer activity, anti-virals, antibiotics or the local delivery of vaccines to the respiratory tract.

Whilst it will often be desired to obtain the composite active particles in dry form, as described above, where the pharmaceutical composition is one comprising a liquid, for example, as propellant, it may be preferable for the active particles to be milled in the presence of that liquid and to omit the drying step, simply using the slurry or suspension of the composite active particles in the liquid as an ingredient in the pharmaceutical composition. Thus for example, where the pharmaceutical composition is for use in a pMDI, the active particles and the additive material may be milled in the presence of liquid propellant (under pressure or at below room temperature if necessary). The resulting slurry may be used directly in a pMDI or further materials may be added, for example, more propellant, surfactants, or co-solvents.

Accordingly, the invention also provides, in one embodiment, a method of making composite active particles for WO 02/43701 PCT/GB01/05315 21 use in a pharmaceutical composition, the method comprising a milling step in which particles of active material are milled in the presence of a liquid and an additive material which is suitable for the promotion of the dispersal of the composite active particles upon actuation of a delivery device.

Preferably, the liquid comprises a propellant suitable for use in a pMDI. Suitable propellants include CFC-12, HFA- 134a, HFA-227, HCFC-22 (difluorochlormethane), HCFC-123 (dicholorotrifluorethane), HCFC-124 (chlorotetrafluoroethane), dimethyl ether, propane, n-butane, isobutane, HFA-125 (pentafluoroethane) and HFA-152 (difluoroethane).

If however, it is desired to isolate the dry composite active particles (or agglomerates thereof) the method may also include a drying step, preferably a spray drying step.

Accordingly, in a further embodiment, the invention provides a method of making composite active particles for use in a pharmaceutical composition, the method comprising a wet milling step in which the particles of active material are milled in the presence of a liquid and an additive material which is suitable for the promotion of the dispersal of the composite active particles upon actuation of a delivery device; and a drying step in which the liquid is removed.

As explained above, the conditions of the drying step, which is preferably a spray drying step, may be chosen either to provide agglomerated composite active particles of a desired size or to provide substantially unagglomerated particles, that is, individual composite active particles.

In some cases it may be preferable to perform the milling step in the absence of liquid, (dry milling). The composite active particles may then be agglomerated by mixing with a liquid and drying to give agglomerated composite active particles.

Accordingly, in a further embodiment, the invention provides a WO 02/43701 PCT/GB01/05315 22 method of making agglomerated composite active particles for use in a pharmaceutical composition, the method comprising: a dry milling step in which particles of active material are milled in the presence of an additive material which is suitable for the promotion of the dispersal of the composite active particles upon actuation of a delivery device; and an agglomeration step, in which the composite active particles are mixed with a liquid and the mixture is dried to remove the liquid.

The invention also provides composite active particles for use in a pharmaceutical composition, preferably a pharmaceutical composition for inhalation, more preferably a powder for a dry powder inhaler.

The invention also provides composite active particles for use in a pharmaceutical composition, each composite active particle comprising a particle of active material and additive material on the surface of that particle of active material, the composite active particles having a mass median aerodynamic diameter of not more than 2ym, the additive material being suitable for the promotion of the dispersal of the composite active particles upon actuation of a delivery device. Preferably, the composite active particles have a MMAD of not more than ljm, especially advantageously not more than 0.54m. As noted above, the composite particles may be in the form of agglomerated composite particles.

MMAD may be determined using an impinger, for example, a multi-stage liquid impinger. Volume median diameters and measurements of the proportion of particles having a diameter less than a certain value may be determined by the Malvern laser light scattering method.

Advantageously, the composite active particles do not comprise significant amounts (more then 10% by weight) of a polymer of a type which would result in the particles becoming sticky. Such polymers include polymers of a alpha- WO 02/43701 PCT/GB01/05315 23 hydroxycarboxylic acid, for example, polylactic acid, copolymers of lactic acid and block copolymers such as ethylene oxide/propylene oxide block copolymers or poloxamines.

The invention further provides a pharmaceutical composition comprising composite active particles.

Preferably, the pharmaceutical composition is a dry powder and is suitable for use in a dry powder inhaler. Such pharmaceutical compositions may comprise essentially only the composite active particles or they may comprise additional ingredients such as carrier particles and flavouring agents.

Carrier particles may be of any acceptable excipient material or combination of materials. For example, the carrier particles may be composed of one or more materials selected from sugar alcohols, polyols and crystalline sugars. Other suitable carriers include inorganic salts such as sodium chloride and calcium carbonate, organic salts such as sodium lactate and other organic compounds such as polysaccharides and oligosaccharides. Advantageously the carrier particles are of a polyol. In particular the carrier particles may be particles of crystalline sugar, for example mannitol, dextrose or lactose. Preferably, the carrier particles are of lactose.

Advantageously, substantially all (by weight) of the carrier particles have a diameter which lies between 20pm and 1000um, more preferably 50pm and 100 m. Preferably, the diameter of substantially all (by weight) of the carrier particles is less than 35Spm and lies between 20gm and 2 Preferably at least 90% by weight of the carrier particles have a diameter between from 60pm to 180pm. The relatively large diameter of the carrier particles improves the opportunity for other, smaller particles to become attached to the surfaces of the carrier particles and to provide good flow and entrainment characteristics and improved release of the WO 02/43701 PCT/GB01/05315 24 active particles in the airways to increase deposition of the active particles in the lower lung.

The ratio in which the carrier particles (if present) and composite active particles are mixed will, of course, depend on the type of inhaler device used, the type of active particles used and the required dose. The carrier particles may be present in an amount of at least 50%, more preferably advantageously 90% and most preferably 95% based on the combined weight of the composite active particles and the carrier particles.

Where carrier particles are included in the pharmaceutical composition, that composition preferably also includes small excipient particles having, for example, a particle size between 5 to 20Am. Preferably the small excipient particles are present in an amount of from 1% to more preferably 5% to 20% based on the weight of the carrier particles.

Compositions for use in a dry powder inhaler which include carrier particles will preferably include at least 2%, more preferably at least 5% and most preferably at least by weight of the composite active particles based on the total mass of the composition. The composite active particles are especially suitable for dry powder compositions which do not include significant amounts of carrier particles and in such compositions the composite active particles will preferably be present in a proportion of at least 60%, more preferably at least 80% by weight based on the total weight of the composition.

The pharmaceutical composition may comprise a propellant and be suitable for use in a pressurised metered dose inhaler.

The invention also provides the use of an additive material as a milling aid in the milling of particles of active material. The term milling aid should be understood to refer to a substance which reduces the amount of energy N required to mill the particles of active material and/or excipient material.

c Throughout this specification, unless the context requires otherwise, the word "comprise", or variations such as "comprises" or "comprising", will be understood to imply the inclusion of a stated element, integer or step, or group of elements, integers or steps, but not the exclusion of any other element, integer or step, or group of elements, integers or steps.

Any discussion of documents, acts, materials, devices, articles or the like which Shas been included in the present specification is solely for the purpose of providing a O context for the present invention. It is not to be taken as an admission that any or all of these matters form part of the prior art base or were common general knowledge in the field relevant to the present invention as it existed in Australia before the priority date of each claim of this application. It will be appreciated by those skilled in the art that numerous variations and/or modifications may be made to the present invention as shown in the specific embodiments without departing from the spirit and scope of the invention as broadly described. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive.

Embodiments of the invention will now be described for the purposes of illustration only with reference to the Figures in which: Figures 1 and 2 are scanning electron micrographs of the composite active particles of Example 1; Figure 3 is a scanning electron micrograph of the composite active particles of Example la; Figure 4 is a scanning electron micrograph of the composite particles of Example 2; Figure 5 is a scanning electron micrograph of the same sample of particles shown in Figure 4 but at a higher magnification; Figure 6 is a scanning electron micrograph of the composite particles of Example 3; Figure 7 is a scanning electron micrograph of the same sample of particles shown in Figure 6 but at a higher magnification; SFigure 8 is a schematic drawing of part of a Mechano-Fusion machine; and Figures 9 and 10 are electromicrographs of composite active particles according to the invention comprising salbutamol sulphate and magnesium stearate in a ratio of 19:1 (Example 4).

SAll percentages are by weight unless indicated otherwise.

C1 Example 1 O 5g of micronised salbutamol sulphate (particle size distribution: 1 to 5 pm) and of magnesium stearate were added to 50cm 3 stainless steel milling vessel together with 20cm 3 dichloromethane and 124g of 3mm stainless steel balls. The mixture was milled at 550 rpm in a Retsch S100 Centrifugal WO 02/43701 PCT/GB01/05315 26 Mill for 5 hours. The powder was recovered by drying and sieving to remove the mill balls. An electron micrograph of the powder is shown in Figure 1. This was repeated 3 times using leucine in place of the magnesium stearate and an electron micrograph of the powder is shown in Figure 2. The powders shown in Figures 1 and 2 appear to have particles in the size range 0.1 to Example la Micronised salbutamol sulphate and magnesium stearate were combined as particles in a suspension in the ratio 10:1 in propanol. This suspension was processed in an Emulsiflex high pressure homogeniser by 5 sequential passes through the system at 25,000 psi. This dry material was then recovered by evaporating the propanol. The particles are shown in Figure 3.

Example 2 It was found that, on drying, the powder prepared in Example 1 including magnesium stearate as additive material formed assemblies of primary particles which were hard to deagglomerate. A sample of this powder was re-dispersed by ball milling for 90 minutes at 550 rpm in a mixture of ethanol, polyvinylpyrolidone (PVPK30) and HFA227 liquid propellant to give the following composition: 0.6% w/w Salbutamol sulphate/magnesium stearate composite particles 0.2% w/w w/w Ethanol 94.2% w/w HFA 227 WO 02/43701 PCT/GB01/05315 27 (The PVP was included to stabilise the suspension of the composite particles in the ethanol/HFA227).

The suspension could be used directly as in a pMDI. In this example, however, the composition was sprayed from a pressurised can through an orifice -0.4mm in diameter to produce dried composite active particles of salbutamol sulphate and magnesium stearate with PVP. Those particles (shown in Figures 4 and 5) were collected and examined and were found to be in the aerodynamic size range 0.1 to 4gm.

Example 3 The process of Example 2 was repeated except that the composition was as follows: 3% w/w Salbutamol sulphate/magnesium stearate composite particles 1% w/w 3% w/w Ethanol 93% w/w HFA 227 The particles produced are shown in Figures 6 and 7.

Example 4 Salbutamol sulphate/magnesium stearate blends a) Homogenised magnesium stearate 240g magnesium stearate (Riedel de Haen, particle size by Malvern laser diffraction:dso 9.74m) was suspended in 2150g dichloroethane. That suspension was then mixed for 5 minutes in a Silverson high shear mixer. The suspension was then processed in an Emulsiflex C50 high pressure homogeniser fitted with a heat exchanger at 10000 psi for 20 minutes in WO 02/43701 PCT/GB01/05315 28 circulation mode (300cm 3 /min) for 20 minutes. The suspension was then circulated at atmospheric pressure for 20 minutes allow it to cool. The next day, the suspension was processed in circulation mode (260cm 3 /min) at 20000psi for 30 minutes.

The dichloroethane was removed by rotary evaporation followed by drying in a vacuum over at 37 0 C overnight. The resulting cake of material was broken up by ball milling for 1 minute.

The homogenised magnesium stearate had a particle size of less than 2pm.

b) A 9:1 by weight blend of salbutamol sulphate and homogenised magnesium stearate having a particle size of less than 2pm was prepared by blending the two materials with a spatula. An electron micrograph of the blended material showed that the blend was mostly in the form of agglomerated particles, the agglomerates having diameters of 50gm and above. The blend was then processed in a Mechano-Fusion mill (Hosokawa) as follows: Machine data: Hosokawa Mechano-Fusion: AMS-Mini Drive: 2.2kW Housing: stainless steel Rotor: stainless steel Scraper: None Cooling: Water Gas purge: None The Mechano-Fusion device (see Figure 8) comprises a cylindrical drum 1 having an inner wall 2. In use, the drum rotates at high speed. The powder 3 of the active and additive particles is thrown by centrifugal force against the inner wall 2 of the drum 1. A fixed arm 4 projects from the interior of the drum in a radial direction. At the end of the arm closest to the wall 2, the arm is provided with a member WO 02/43701 PCT/GB01/05315 29 which presents an arcuate surface 6, of radius of curvature less than that of inner wall 2, toward that inner wall. As the drum 1 rotates, it carries powder 3 into the gap between arcuate surface 6 and inner wall 2 thereby compressing the powder. The gap is of a fixed, predetermined width A. A scraper (not shown in Figure 8) may be provided to scrape the compressed powder from the wall of the drum.

All samples were premixed for 5 minutes by running the machine at 1000rpm. The machine speed was then increased to 5050rpm for 30 minutes. The procedure was repeated for salbutamol sulphate/magnesium stearate in the following weight ratios: 19:1, 3:1, 1:1.

Electronmicrographs of the 19:1 processed material are shown in Figures 9 and 10 and indicate that the material was mostly in the form of simple small particles of diameter less than 5gm or in very loose agglomerates of such particles with only one agglomerate of the original type being visible.

The 3:1 and the 19:1 blends were then each loaded into a capsule and fired from a twin stage impinger. A sample of unprocessed salbutamol sulphate was also fired from the TSI to provide a comparison.

The fine particle fractions were then calculated and are given in table 1.

Composition Fine Particle Fraction salbutamol sulphate 28 salbutamol sulphate/magnesium 66 stearate 19:1 salbutamol sulphate/magnesium 66 stearate 3:1 Table 1: Fine Particle Fraction results for salbutamol sulphate blends.

WO 02/43701 PCT/GB01/05315 30 Example Micronised glycopyrrolate and homogenised magnesium stearate (as described in Example 4) were combined in a weight ratio of 75:25. This blend (~20g) was then milled in the Mechano-Fusion AMS-Mini system as follows. The powder was pre-mixed for 5 minutes at ~900rpm. The machine speed was then increased to ~4,800rpm for 30 minutes. During the milling treatment the Mechano-Fusion machine was run with a 3mm clearance between element and vessel wall, and with cooling water applied. The powder of composite active particles was then recovered from the drum vessel.

The experiment was repeated using the same procedure but the active particle and homogenised magnesium stearate were combined in the ratio 95:5, and milled for 60 minutes at 4,800rpm.

This above process was repeated using the same procedure with a sample of sodium salicilate as a model drug and homogenised magnesium stearate in the ratio 90:10, where the sodium salicilate had been produced as approximately micron sized spheres by spray drying from a Buchi 191 spray dryer.

It was believed that the spherical shape of these particles may be advantageous in the coating process. Milling was for minutes at 4,800rpm.

Claims (21)

1. A method for making composite active particles for use in a pharmaceutical composition for pulmonary administration, the method comprising a milling step in which particles of active material are milled in the presence of particles of an additive material _so as to ensure a sufficient break-up of agglomerates of both active material and additive material, dispersal and even distribution of the additive material over the active material, and so that the particles of additive material become fused to the surface of the N particles of active material, wherein the additive material is suitable for the promotion of O Othe dispersal of the composite active particles upon actuation of an inhaler.
2. The method according to claim 1, wherein the milling step involves compressing a mixture of the active particles and additive particles in a gap of predetermined width.
3. The method according to claim 2 in which the gap is not more than 10mm wide.
4. The method according to any one of claims 1 to 3, wherein mass median aerodynamic diameter (MMAD) of the particles of active material is substantially reduced during the milling step. The method according to any one of claims 1 to 4, wherein mass median aerodynamic diameter (MMAD) of the particles of additive material is substantially reduced during the milling step.
6. The method according to claim 4 or 5, wherein, after the milling step, the mass median aerodynamic diameter (MMAD) of the composite active particles is not more than
7. The method according to any one of claims 1 to 6, which also comprises, after the milling step, a processing step in which the degree of aggregation of the composite active particles is changed.
8. The method according to claim 7, wherein the processing step is an agglomeration step.
9. The method according to claim 7, wherein the processing step is a deagglomeration step. The method according to any one of the preceding claims, wherein, after the milling step, liquid is added, followed by a drying step in which a mixture of the composite active particles and the liquid is dried to remove the liquid.
11. The method according to claim 10, wherein, in the drying step, the composite active particles agglomerate to form agglomerated composite active particles.
12. The method according to claim 10 or claim 11, wherein the drying step is a spray drying step. (13. The method according to claim 10 or claim 11, wherein in the drying step the liquid is evaporated slowly.
14. The method according to claim 10 or claim 11, wherein the drying step is a freeze drying step. The method according to any one of claims 1 to 14, wherein the additive material comprises an amino acid.
16. The method according to any one of claims 1 to 14, wherein the additive material comprises a phospholipid. S 17. The method according to any one of claims 1 to 14, wherein the additive material comprises a metal stearate.
18. Composite active particles for use in a pharmaceutical composition as made by the method according to any one of claims 1 to 17.
19. Composite active particles for use in a pharmaceutical composition for pulmonary administration, each composite active particle comprising a particle of active material and additive material dispersed, evenly distributed and fused on the surface of that particle of active material, the composite active particles having a mass median aerodynamic diameter of not more than 10pm and the additive material being suitable for the promotion of the dispersal of the composite active particles upon actuation of a delivery device. Composite active particles according to claim 18 or claim 19, which are in the form of agglomerated composite active particles.
21. Composite particles according to any one of claims 18 to 20, in which the additive particles form a coating on the surface of the particles of active material.
22. Composite active particles according to claim 21, wherein the coating is a discontinuous coating.
23. Composite active particles according to claim 21 or claim 22, wherein the coating is not more than 1lpm thick.
24. A pharmaceutical composition comprising composite active particles as made by a method according to any of claims 1 to 17 or composite active particles according to any one of claims 18 to 23. The pharmaceutical composition according to claim 24, which is a dry powder and is suitable for use in a dry powder inhaler.
26. The pharmaceutical composition according to claim 24, which comprises a propellant and is suitable for use in a pressurised metered dose inhaler.
27. A method of making composite active particles for use in a pharmaceutical composition substantially as described herein.
28. Composite active particles for use in a pharmaceutical composition substantially as described herein. Dated this 14 h day of July 2006. VECTURA LIMITED C Patent Attorneys for the Applicant: SALLENS ARTHUR ROBINSON O Patent Trade Marks Attorneys
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GB0030946A GB0030946D0 (en) 2000-12-19 2000-12-19 Method of making particles for use in a pharmaceutical composition
GB0030946.8 2000-12-19
WOPCT/GB01/01606 2001-04-09
PCT/GB2001/001606 WO2001076575A2 (en) 2000-04-07 2001-04-09 The treatment of respiratory diseases
GB0124010A GB0124010D0 (en) 2001-10-05 2001-10-05 Pharmaceutical compositions for inhalation
GB0124010.0 2001-10-05
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